| HS Code | 686008 |
| Density | 0.921 g/cm³ |
| Melt Flow Rate | 2.5 g/10 min (190°C/2.16 kg) |
| Melting Point | 120 °C |
| Vicat Softening Point | 95 °C |
| Tensile Strength At Yield | 10 MPa |
| Tensile Strength At Break | 25 MPa |
| Elongation At Break | 700% |
| Flexural Modulus | 250 MPa |
| Shore D Hardness | 50 |
| Haze | 7% |
| Gloss | 85 |
| Dart Impact | 150 g |
| Elmendorf Tear Strength Md | 120 g |
| Elmendorf Tear Strength Td | 200 g |
| Seal Initiation Temperature | 90 °C |
| Hot Tack Strength | High |
| Low Temperature Brittleness | < -70 °C |
| Molecular Weight Distribution | Narrow |
As an accredited Mitsui Chemicals Evolue mLLDPE SP2530S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Mitsui Chemicals Evolue mLLDPE SP2530S is supplied in 25 kg paper bags, typically 40 bags per pallet. |
| Container Loading (20′ FCL) | Mitsui Chemicals Evolue mLLDPE SP2530S supplied in 25 kg bags, palletized and loaded into a 20-foot FCL container for export. |
| Shipping | Mitsui Chemicals Evolue mLLDPE SP2530S is shipped as non-hazardous polyethylene resin pellets, typically in moisture-barrier 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. Use clean, dry containers/trucks; keep cool, dry, and protected from sunlight, heat, and contamination. No special hazardous cargo classification. |
| Storage | Store Mitsui Chemicals Evolue mLLDPE SP2530S in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and ignition sources. Keep original bags/containers closed and off the floor to prevent moisture, dust, and contamination. Avoid prolonged high temperatures and excessive stacking that may deform packaging. Follow the supplier SDS and local regulations. |
| Shelf Life | Store in a cool, dry, well-ventilated area; shelf life is typically 24 months from manufacture when unopened. |
In high-speed vertical form-fill-seal packaging lines operating between 100 packages/min and 160 packages/min, the sealant web is required to develop hot tack within 0.10–0.20 s of seal jaw contact and retain acceptable peel resistance at temperatures above the crystalline softening point. Mitsui Chemicals Evolue mLLDPE SP2530S is a metallocene-catalysed ethylene/α-olefin copolymer with a melt flow rate of 2.0 g/10 min at 190°C under 2.16 kg load as measured by ISO 1133-1, and a density of 0.923 g/cm³ as measured by ISO 1183-1. The narrow comonomer distribution reduces the seal initiation temperature relative to Ziegler-Natta C4-LLDPE of equivalent density; this property is exploited in a three-layer cast film where the sealant layer is formulated at 70 wt% SP2530S and 30 wt% of a 0.918 g/cm³ low-density polyethylene with a 4.0 g/10 min melt flow rate. The LDPE component lowers melt elasticity at the die lip and prevents draw resonance on lines fitted with a 90 mm barrier-screw extruder having a 30:1 L/D ratio. On production-scale cast film equipment, the die gap is set at 0.8–1.0 mm; gaps beyond 1.2 mm increase neck-in and produce transverse gauge deviation above ±6% without a vacuum box correction. The chill roll is held at 18–22°C, air knife velocity is 5–8 m/s, and the vacuum box pressure is 2–4 kPa. Pre-drying of the resin is not required when pellets are stored at less than 60% relative humidity; surface moisture above that threshold can generate micro-voids in film below 30 µm, and may require desiccant drying at 80°C for 2 h if condensation is visible during transport. The finished sealant web is corona-treated to 42–46 mN/m under ASTM D2578 before lamination or printing. Food-contact compliance is established under FDA 21 CFR 177.1520 for olefin polymers and Regulation (EU) No 10/2011; overall migration is controlled below 10 mg/dm² in the relevant food simulants. Hot tack is measured by ASTM F1921 and heat-seal strength by ASTM F88 on a 65 µm pillow pack for frozen vegetables. At seal jaw temperatures above 140°C, low-molecular-weight fractions may transfer to Teflon-coated sealing jaws and produce char accumulation during line stoppages longer than 30 s. The terminal product is an opaque white 65 µm cast film bag sealed at 125–135°C with a dwell time of 0.1–0.2 s.
| Standard or regulation | Scope or clause | Operational limit |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Conditions of Use A through H |
| Regulation (EU) No 10/2011 | Plastics intended for food contact; Annex I authorised monomers | Overall migration limit 10 mg/dm² |
| GB 4806.6-2016 | Food contact plastic resins and articles | Overall migration limit 10 mg/dm² |
Heavy-duty liners for chemical and resin packaging are produced on three-layer blown film lines fitted with a 250 mm die, internal bubble cooling, and automatic gauge control. SP2530S is formulated at 85 wt% with 15 wt% of a 0.955 g/cm³ high-density polyethylene to increase modulus and reduce creep at the bottom seal. The screw configuration is a 25:1 L/D single screw with a Maddock mixing section, and the melt temperature at the die is held at 200–215°C. Melt pressure upstream of the screen pack normally ranges from 35–50 MPa; a pressure differential across the 60/80/100 mesh screen pack above 15 MPa indicates gel accumulation and requires screen replacement. The bubble is operated at a blow-up ratio of 2.0–3.0; BUR values above 3.0 induce flutter at the frost line when the internal bubble pressure differential exceeds 2 kPa. Frost line height is set between 450 mm and 650 mm. A frost line below 450 mm increases blocking in the collapsing frame, while a frost line above 650 mm reduces machine-direction tear resistance because of higher orientation before solidification. Trim derived from edge slitting is re-introduced at 0–20 wt%; above 20 wt%, melt pressure fluctuations above ±5% produce visible gauge bands. Published formulation data for this specific SP2530S/HDPE blend is limited, but production-scale observations on 90 mm grooved feed extruders show that feed throat bridging is more frequent when the reclaim fraction contains dusty fines and the hopper is not fitted with a pneumatic bridge breaker. The liner is inflated to a layflat width of 1300 mm at a gauge of 150 µm, and both dart impact and Elmendorf tear are measured under ASTM D1709A and ASTM D1922 to confirm mechanical resistance. Compliance for non-food chemical goods is limited to REACH and RoHS 2011/65/EU; no food-contact declarations apply unless the film is separately tailored to FDA 21 CFR 177.1520. The terminal article is a 150 µm liner used inside 25 kg corrugated boxes for hygroscopic resin export.
| Parameter | Working range | Failure outside range |
|---|---|---|
| Die melt temperature | 200–215°C | Melt pressure rise below 200°C; oxidative degradation above 215°C |
| Blow-up ratio | 2.0–3.0 | Bubble flutter above 3.0; transverse tear loss below 2.0 |
| Frost line height | 450–650 mm | Blocking below 450 mm; MD tear reduction above 650 mm |
| Reclaim content | 0–20 wt% | Gauge bands and gel accumulation above 20 wt% |
When pallet unitization requires a 23 µm cast stretch film with a pre-stretch ratio of 200% on a 70 mm 30:1 L/D line, SP2530S is assessed for tear propagation and puncture resistance rather than for heat-seal behaviour. The casting formulation contains 92 wt% SP2530S and 8 wt% of a polyisobutylene-based cling masterbatch added through a gravimetric feeder at the main feed throat. The cling masterbatch depresses melt viscosity; therefore, the extruder melt temperature is reduced from 230°C to 215°C in the first trials, and die pressure is monitored for a 10–15% reduction before the screw speed is increased. The cast die is a 1400 mm coat-hanger slot die with a 0.7 mm lip gap, and the chill roll is kept at 15–18°C with a vacuum box at 3–5 kPa to ensure contact. The film passes through a pre-stretch unit set to 200% elongation and is wound on a centre surface winder at 80–120 m/min. Line speeds above 150 m/min can induce transverse thickness bands if die lip temperature varies by more than ±3°C; this failure mode is corrected with segmented die heaters and an internal deckle. Cling force is measured by ASTM D5458, puncture resistance by ASTM D5748, and Elmendorf tear by ASTM D1922 in the machine direction and transverse direction. The cling masterbatch migrates to the film surface over 24–48 h after winding; therefore, cling force is not certified immediately after slitting. Published data for this specific SP2530S and polyisobutylene cling masterbatch formulation is limited; production-scale trials are required to fix the final die pressure and pre-stretch settings because the cling additive changes the melt relaxation spectrum. Compliance is limited to REACH and RoHS 2011/65/EU; no food-contact claim is made. The terminal product is a 500 mm wide machine-grade pallet wrap with an effective post-stretch gauge of 23 µm and a roll length verified by gravimetric methods.
In dry food stand-up pouches, a 30 µm cast film produced from SP2530S is adhesive-laminated to a 12 µm biaxially oriented polyethylene terephthalate outer ply and a 9 µm aluminium foil barrier ply, leaving the SP2530S layer as the innermost heat-seal surface. The SP2530S film is run at 100 wt% virgin resin because reclaimed material increases the gel count and reduces seal consistency on jaws closing at 40–45 cycles/min. The film is cast on a 65 mm single-screw extruder with a 25:1 L/D ratio at a melt temperature of 220°C, a die gap of 0.8 mm, and a chill roll temperature of 20°C. Antiblock masterbatch is added at 0–2 wt% for gusseted pouch formats; above 2 wt%, seal strength measured by ASTM F88 falls and whisper fissures appear at the gusset fold during drop testing. Flat three-side seal pouches can tolerate 3 wt% antiblock without seal failure. The solventless lamination step is carried out at 2.0–2.5 g/m² adhesive coat weight, followed by 24 h of cure at 35°C before pouch conversion. The seal initiation temperature of the SP2530S ply permits jaw settings of 130°C at 0.2 s dwell; the hot-tack window is verified by ASTM F1921 because stand-up pouch jaws close at 40–45 cycles/min and the pouch is released before the seal has fully crystallized. Compliance is established under Regulation (EU) No 10/2011 and GB 4806.6-2016 for food contact; overall migration is below 10 mg/dm². The terminal article is a gusseted stand-up pouch with a 150 g dry food fill mass, validated for a 1.0 m drop height at both 20°C and 0°C after filling and sealing. The SP2530S layer is not recommended for retort or hot-fill above 90°C because the seal strength decay rate above that threshold is not covered by standard pouch validation data for this configuration.
Silage conservation films in the 0.15–0.25 mm gauge range require a balance of puncture resistance, tear propagation, and UV weathering in a three-layer blown film. SP2530S is compounded into the core layer at 95 wt% with 5 wt% of a HALS/UV absorber masterbatch based on a polyolefin carrier; the additive is pre-dried at 60°C for 4 h if storage humidity exceeds 60% RH to avoid hydrolysis of the carrier. The blown film line is configured with a 400 mm three-layer die, internal bubble cooling, and a rotating haul-off. The melt temperature is maintained at 210–220°C; the blow-up ratio is 2.2, and the frost line height is controlled at 500–600 mm to balance machine-direction and transverse-direction tear. The output is set to 300 kg/h on a 105 mm main extruder; line speed is adjusted to produce a nominal gauge of 0.20 mm. Thickness variation is kept below ±8% by means of capacitive reverse profile control; deviation above ±10% produces weak points at folded corners when the silage sheet is stretched over the clamp. The UV stabiliser dispersion is checked by oxidative induction time under ISO 11357-6; the target OIT is greater than 20 min at 210°C in the finished film, and values below 15 min indicate poor masterbatch dispersion or insufficient letdown ratio. Puncture resistance is measured by ASTM D4833, and dart impact by ASTM D1709A. Compliance is limited to REACH and no food-contact claim is made; the film is marketed as a silage clamp sheet with a width of 12 m and a length of 50 m for agricultural conservation of grass and maize silage. Reclaimed edge trim is not re-introduced into this film at levels above 10 wt%, because UV-stabilised reclaim raises gel accumulation on the screen pack and increases pressure differential beyond 12 MPa within 4 h of continuous operation.
For individually quick-frozen seafood packed at -25°C, the sealant layer must resist puncture from ice crystal edges and maintain seal integrity through thaw cycles when protein exudate contacts the inner surface. A coextruded cast film with SP2530S as the sealant ply is produced on a 900 mm three-layer cast line with a 75 mm skin extruder and a 45 mm core extruder. The sealant layer is formulated at 80 wt% SP2530S and 20 wt% of a 0.924 g/cm³ LDPE to improve sealing at low temperatures; the core layer contains a white concentrate for opacity and UV screening of the freezer environment. The die gap is 0.9 mm, the chill roll is held at 18°C, and the air knife is set at 6 m/s. The film is printed and laminated to a reverse-printed PET outer ply before pouching. Seal strength is measured by ASTM F88 at 23°C and after 30 min at -25°C; low-temperature seal strength is often the critical rejection criterion because crystalline stiffening reduces the peel energy absorbed before fracture. Puncture resistance is measured by ASTM D5748 at -25°C. Food-contact compliance is covered by FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011, with overall migration below 10 mg/dm². The terminal article is a 50 µm frozen seafood pouch with a fill mass of 1 kg, packed on a vertical form-fill-seal machine at 60–80 packs/min. At packaging speeds above 80 packs/min, the seal dwell time falls below 0.1 s and the sealant layer may fail to develop sufficient hot tack; therefore, the line is restricted to 60–80 packs/min for this gauge and film structure.
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Mitsui Chemicals Evolue SP2530S is a metallocene linear low-density polyethylene supplied in pellet form for extrusion lamination and sealant-web coextrusion. Manufacturer-published nominal values place the melt flow rate at 2.0 g/10 min when measured at 190 °C under 2.16 kg load in accordance with ASTM D1238 and ISO 1133-1:2022, and the density at 0.925 g/cm³ when measured at 23 °C in accordance with ASTM D1505 and ISO 1183-1:2019. The S suffix is used by the producer to indicate a slip/antiblock-containing formulation; the exact additive package and batch-to-batch concentrations must be read from the certificate of analysis. The resin belongs to the ethylene–higher α-olefin copolymer class, typically a 1-hexene comonomer in the Evolue mLLDPE family, and is manufactured using a metallocene catalyst system. Compared with broad-molecular-weight-distribution Ziegler-Natta butene LLDPE of equivalent density and melt index, the narrow molecular weight distribution and more uniform comonomer incorporation alter seal initiation, hot tack, toughness, and optical performance in cast and extrusion-coated film.
Specification compliance for SP2530S should be verified against the producer’s technical datasheet and the batch certificate of analysis. The two primary polymer-level anchors are the melt flow rate and density. Secondary values that are commonly reported for mLLDPE film grades include the DSC melting peak, tensile properties, and film optics; for SP2530S, published data for many of these secondary endpoints is limited, so direct production trials remain necessary. The following table records the polymer-level values and the standard designations that govern them.
| Property | Nominal value | Test method |
|---|---|---|
| Melt flow rate | 2.0 g/10 min | ASTM D1238, ISO 1133-1:2022 |
| Density | 0.925 g/cm³ | ASTM D1505, ISO 1183-1:2019 |
| Comonomer type | Ethylene–1-hexene | Producer technical datasheet |
| Additive package | Slip/antiblock | Producer certificate of analysis |
For film testing, the following methods apply: tensile properties on 25 mm wide specimens at 500 mm/min following ASTM D882 or ISO 527-3; dart impact using ASTM D1709 Method A or B with a 38 mm diameter dart; Elmendorf tear using ASTM D1922; seal strength using ASTM F88/F88M with a 25.4 mm specimen and dwell conditions recorded; hot tack using ASTM F1921; coefficient of friction using ASTM D1894; and haze and gloss using ASTM D1003 and ASTM D2457. The melting peak of an ethylene–hexene copolymer at 0.925 g/cm³ density typically falls near 121–123 °C by ASTM D3418, but the producer-specific value controls.
On a 90 mm single-screw extrusion coating line with an L/D of 30:1, a barrier screw, and a 1200 mm coathanger die, grade-specific trials for SP2530S commonly start with barrel temperatures from 180 °C at the feed throat to 290 °C at the adapter, with die temperatures held between 290 °C and 310 °C. The published grade-specific processing window for SP2530S is limited; these starting values are derived from converter practice for metallocene LLDPE sealant layers and must be confirmed against the producer’s extrusion guide. Melt temperature should be measured by an immersion thermocouple at the die lip, not inferred from barrel setpoints. Because the resin has a narrower molecular weight distribution than Ziegler-Natta grades, shear viscosity is less responsive to increasing screw speed; die pressure should be monitored to avoid over-pressurization of the die body. A short air gap, typically 150–250 mm, reduces neck-in and melt-curtain oscillation, but an air gap below 100 mm can restrict melt oxidation and reduce adhesion to aluminum foil or primed substrates. Chill roll temperatures from 15 °C to 25 °C are standard for quenching; higher chill roll temperatures reduce optical gloss and increase blocking risk.
Neck-in is typically greater for mLLDPE than for LDPE at the same melt temperature and air gap. On a 1200 mm die, total neck-in of 40–80 mm per side may be observed depending on melt temperature, air gap, line speed, and die lip opening. Edge bead formation should be controlled by die deckle position and secondary cooling. Draw resonance may appear at line speeds above 120–150 m/min; suppression requires raising melt temperature within the 270–310 °C window, shortening the air gap, or increasing melt curtain tension within the limits of the substrate. At melt temperatures above 320 °C, oxidative chain scission can generate gel particles, odor, and die-lip build-up. Residence time at melt temperature should be kept below 30 min during stoppages, and the screw should be purged with a lower-viscosity polyethylene before shutdown.
For extrusion lamination to aluminum foil or metallized films, converter practice often introduces ozone into the air gap at 0.5–1.5 g/h per meter of web width to increase polar functionality and improve wetting. Direct adhesion should be evaluated by peel testing after lamination and curing, using TAPPI T 540 or an equivalent aluminum-foil peel method. If the structure includes paper or oriented polyester, corona pre-treatment of the substrate at 38–44 mN/m is commonly applied; the actual dyne level must be verified because storage conditions and additives influence decay.
The replacement value of SP2530S over conventional Ziegler-Natta butene LLDPE is primarily seen in the sealant layer of coextruded polyethylene films and extrusion-laminated pouches. A metallocene-catalyzed ethylene–hexene structure with a density of 0.925 g/cm³ typically produces a lower heat seal initiation temperature and a broader hot-tack plateau than a butene LLDPE of the same density and 2.0 g/10 min melt index. In published comparative studies, metallocene LLDPE grades of this density class show a reduction in heat seal initiation temperature of approximately 5–15 °C relative to conventional butene copolymers; the exact difference for SP2530S must be measured against the control grade using ASTM F2029 for heat seal initiation and ASTM F1921 for hot tack.
Seal-strength testing per ASTM F88/F88M should record dwell time, pressure, and anvil temperature. Typical laboratory conditions for monolayer sealant films are 0.5 s dwell, 0.275 MPa applied pressure, and 25.4 mm specimen width. The measured seal strength depends on film thickness, coextruded backings, and the fusion of the sealant layer to the substrate; comparative statements without these variables are not technically meaningful.
When compared with LDPE extrusion-coating grades in the same converter, SP2530S generally provides higher dart impact and Elmendorf tear at equivalent gauge, but exhibits greater neck-in and lower melt strength. LDPE remains the preferred outer layer when high-speed draw-down and low neck-in are dominant. Within the Evolue mLLDPE range, lower-density variants with density near 0.915–0.920 g/cm³ reduce flexural modulus and seal initiation temperature further, while higher-density variants near 0.930 g/cm³ increase stiffness but may raise seal initiation temperature. SP2530S occupies the intermediate region where 0.925 g/cm³ density provides enough modulus for lamination webs while retaining sealant-layer performance. Compared with metallocene octene LLDPE of similar density, hexene grades may show slightly lower toughness but are widely used where a balance of processability and sealability is required; published data for this specific SP2530S comparison is limited.
The metallocene catalyst used for this product class typically yields a molecular weight distribution, expressed as Mw/Mn, near 2.0–2.5, while conventional Ziegler-Natta butene LLDPE of the same melt index often exhibits Mw/Mn in the range 3.5–4.5 when measured by high-temperature GPC. This difference explains the shear-thinning behavior and can require changes in extruder screw speed and die gap. The narrow distribution also produces a lower extractable fraction than conventional LLDPE because there are fewer very-low-molecular-weight chains. Extraction testing per FDA 21 CFR 177.1520 or EU Regulation (EU) No 10/2011 should be based on the finished film structure rather than the pellet. In practice, hexane extractable values for metallocene LLDPE of this density class are often below 1.0 wt%, but the grade-specific certificate of analysis should be used because the additive package can influence the result.
The S suffix indicates that the grade is supplied with slip and antiblock additives. Slip additives based on unsaturated fatty acid amides migrate to the film surface over time; coefficient of friction is therefore time- and temperature-dependent. Measurements should follow ASTM D1894 after conditioning at 23 °C and 50% RH for at least 24 h, and repeated after 48 h because migration kinetics can shift the kinetic coefficient by 0.1–0.3. Blocking is measured by ASTM D3354; blocking force increases with winding tension, storage temperature above 40 °C, and contact time. The antiblock component, typically a mineral such as silica, raises haze and may reduce gloss at high addition levels. For SP2530S, the producer’s formulated package is intended to balance film handling and clarity, but if the converter adds additional slip/antiblock masterbatch, the final mixture must be re-tested because the additive concentration no longer matches the producer’s specification.
Die-lip build-up is a common production-scale failure mode when oxidized low-molecular-weight species accumulate at the die exit during long runs. On a coater running SP2530S at 290–310 °C, visible die-lip deposits may begin after 6–10 h depending on melt temperature, air gap, and purging discipline. Periodic die wiping or use of a fluoropolymer die-lip release coating reduces the frequency of edge tear and melt-curtain breaks. Winding-induced blocking is another observed limitation; corona-treated films should be wound at tapered tension below 120 N/m and cooled before storage to prevent blocking defects. These observations are derived from general mLLDPE converter experience rather than published SP2530S case studies.
| Regulatory document | Designation | Verification requirement |
|---|---|---|
| US FDA olefin polymer | 21 CFR 177.1520 | Producer food-contact statement; end-use conditions |
| EU food-contact plastics | Regulation (EU) No 10/2011 | Overall migration ≤ 10 mg/dm²; specific migration limits for additives |
| EU chemical regulation | Regulation (EC) No 1907/2006 | REACH registration and SVHC confirmation |
| EU hazardous substances in EEE | Directive 2011/65/EU | No intentional Pb, Cd, Hg, Cr VI, PBB, PBDE at homogeneous material level |
The grade is typically supplied with a food-contact statement referencing FDA 21 CFR 177.1520 for olefin polymers and Commission Regulation (EU) No 10/2011 on plastic materials intended to come into contact with food. Compliance under the EU regulation is not a single resin property; the finished laminate must meet an overall migration limit of 10 mg/dm² and specific migration limits for each additive. Fatty acid amide slip additives and inorganic antiblock agents are subject to specific migration limits in some jurisdictions. REACH registration under Regulation (EC) No 1907/2006 and absence of RoHS-restricted substances under Directive 2011/65/EU should be confirmed through the producer’s regulatory declaration. The resin is not intended for medical implant, parenteral, or continuous steam sterilization applications unless separately validated by the converter. Pre-drying is not required under normal storage conditions, but condensation on cold pellets should be avoided. Storage above 50 °C and direct sunlight should be avoided to prevent additive migration and pellet blocking.